US2521913A - Process for acylating enolizable organic compounds - Google Patents

Process for acylating enolizable organic compounds Download PDF

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US2521913A
US2521913A US25525A US2552548A US2521913A US 2521913 A US2521913 A US 2521913A US 25525 A US25525 A US 25525A US 2552548 A US2552548 A US 2552548A US 2521913 A US2521913 A US 2521913A
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acid
acetate
acylating
acetoxy
organic compounds
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Jr Hugh J Hagemeyer
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Eastman Kodak Co
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Eastman Kodak Co
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C69/00Esters of carboxylic acids; Esters of carbonic or haloformic acids
    • C07C69/66Esters of carboxylic acids having esterified carboxylic groups bound to acyclic carbon atoms and having any of the groups OH, O—metal, —CHO, keto, ether, acyloxy, groups, groups, or in the acid moiety
    • C07C69/73Esters of carboxylic acids having esterified carboxylic groups bound to acyclic carbon atoms and having any of the groups OH, O—metal, —CHO, keto, ether, acyloxy, groups, groups, or in the acid moiety of unsaturated acids
    • C07C69/732Esters of carboxylic acids having esterified carboxylic groups bound to acyclic carbon atoms and having any of the groups OH, O—metal, —CHO, keto, ether, acyloxy, groups, groups, or in the acid moiety of unsaturated acids of unsaturated hydroxy carboxylic acids
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C67/00Preparation of carboxylic acid esters

Description

Patented Sept. 12, 1950 PROCESS FOR ACYLATING ENOLI ZABLE ORGANIC COMPOUNDS Hugh J. Hagemeyer, Jr., Kingsport, Tenn., as-
signor to Eastman Kodak Company, Rochester, N. Y., a corporation of New Jersey No Drawing. Application May e, 1948, Serial No. 25,525
7 Claims. (01. 260-484) This invention relates to a process for acylating enolizable organic compounds.
It is known that ketene (CH2=C=O) and substituted ketenes will react with certain aldehydes and ketones, in the presence of an acid catalyst, to give unsaturated carboxylic esters. For example, ketene can be reacted with ketones, in the presence of hydrochloric, phosphoric or sulfuric acids, to give isoalkenyl acetates of the type represented by isopropenyl acetate. See U. S. Patent 2,383,965 to Gwynn and Degering, dated September 4, 1945. Likewise, it is known that ketene can be reacted with ketoesters and diketones, in the presence of an acid catalyst containing the group -SO2OH (e. g. sulfuric acid, a halogenasulfonic acid such as chlorosulfonic acid, an alkylsulfuric acid such as methylsulfuric acid or a sulfamic acid such as sulfaminic acid) to produce enol acetates of these compounds, of which ethylacetoacetate and acetylacetone are typical. See U. S. Patents 2,407,301 and 2,407,302 to Spence and Degering, dated September 10, 1946. Unsaturated carboxylic esters have also been prepared by reacting ketene with aldehydes and ketones in the presence of still other acid catalysts such as p-toluene-sulfonic acid, sulfoacetic acid (I-IO-SO2-CH2COOH) or addition compounds formed in situ such as the sulfoacetic acid-acid addition product (CHsCOOI-I.HO-SO2CH:COOH) While the above-mentioned processes are capable of providing various useful unsaturated carboxylic esters, considerable polymerization occurs in the reactions. For example, ketene (CH2=C=O) is an unstable material and has a decided tendency to polymerize to diketenes and dehydroacetic acid and to decompose under the influence wherein R and R1 each represents an alkyLan' aralkyl or an aryl group, in the presence of a com plex acid catalyst, for example, an acyl sulfocarboxylic acid, unsaturated carboxylic esters are obtained at a much faster rate and in markedly increased yields with little, if any, objectionable by-products. Typical ofsuch complex acid catalysts is acetyl sulfoacetic acid H-D-CO-O-S'O2D1-COOH wherein D and D1 are divalent saturated aliphatic hydrocarbon groups (i. e. alkylene groups of the series CnHzn wherein n is a whole number not greater than 3) of 'the same number of carbon atoms selected from those containing from 1 to 3 carbon atoms such as, for example, acetyl sulfoacetic acid, propionyl sulfopropionic acid or butyryl sulfobutyric acid.
It is, accordingly, an object of the invention to provide an improved process, wherein the abovedefined acid catalysts are employed, for preparing unsaturated carboxylic esters. Other objects will become apparent hereinafter.
In accordancewith the invention, the unsaturated monocarboxylic ester is reacted with the enolizable organic compound, in the presence of the complex acid catalyst and at an elevated temperature, and the enol ester product then separated as by fractional distillation. Where the enolizable organic compound has a boiling point 40"; above that of the ketone by-product, the acetylation can conveniently be carried out in an ordinary distillation arrangement. As the acylation proceeds, the ketone is flashed off, thereby forcing the reaction to completion. This type of reaction" is illustrated with isopropenyl acetate and crotonaldehyde which react to form l-acetoxy butadiene-l,3 and acetone. The enolizable organic compound to be acylated may be diluted with an inert solvent such as diisopropyl ether, benzene, carbon tetrachloride, carbon disulfide,
ethylene dichloride, etc., and the reaction con-3 ducted in this diluted medium. The temperature of the reaction can be varied from to C. The concentration of the catalyst can be varied from 0.05 to 3.0 per cent by weight of the reactants. Higher catalyst concentrations may be used, but no additional advantage would result. The reaction may be carried out at reduced, normal or increased pressures, either in batchwise or in continuous operations. The ratio of the unsaturated carboxylic ester acylating agent to the enolizable organic compound can be varied widely in the reaction, since any amount of the acylating agent will react to give a quantity of the product, but advantageously from 1 to 5 molecular proportions of the unsaturated monocarboxylic ester to each molecular proportion of the enolizable organic compound may be used. Polymerization inhibitors such as copper acetate, hydroquinone, etc., can be advantageously added to the reaction mixtures. Advantageously, the catalyst can be neutralized by addition to the reaction mixture, just prior to the product-separation step, of an appropriate amount of a neutralizing reagent such as sodium acetate, sodium bicarbonate, sodium hydroxide and the like.
Typical of the unsaturated monocarboxylic esters which I employ as acylating agents in practicing my invention are: isopropenyl acetate (2-acetoxy-propene-l) 2-acetoxy-butene-1,2- acetoXy-pentene-l, 2-acetoxyhexene-l, 2-acetoxyheptene-l, 2-(chloroaoetoxy) -hexene-1, 2- benzoyloxyhexene-l, c-acetoxystyrene, 2-(phenylacetoxy) -propene-1, 2-acetoxy-3-phenylpropene-l, etc. Such unsaturated esters in which the acid radical is an acetate radical (i. e. acetoxy derivatives) can be prepared by condensing the appropriate ketone with ketene, in the presence of sulfuric acid. See Gwynn and Degering, Jour. Chem. Soc. 64 2216 (1942). See also my copending application Serial No. 25,526, filed of even date herewith (now United States Patent 2,476,860, dated July 19, 1949). All the unsaturated monocarboxylic esters can be prepared by adding a monocarboxylic acid (e. g. acetic acid, propionic acid, butyric acid, benzoic acid, etc.) to the appropriate monosubstltuted acetylene, in the presence of boron trifluoride. See Henion and Nieuwland, Journal of the Am. Chem. Soc. 56 1802 (1934).
'Suitable enoliz'abl'e organic compounds which may be employed in the process of the invention are 'aldehydes which contain at least two carbon atoms and which contain at least one hydrogen atom on the carbon atom adjacent the carbonyl group. The aldehydes containing at least two hydrogen atoms on the carbon atom adjacent the aldehyde group are especially useful in practicing the invention. Aldehydes which contain a system of conjugated bonds in which the double bond of the aldehyde group is a part such as, for example, crotonaldehyde, z-ethacrolein and 2-ethyl-2-hexenal are also adaptable to the process of the invention. Acrolein and Z-methacrolein cannot be employed in my process. Polymeric forms of the aldehydes can be employed. Other enolizable organic compounds which may likewise be employed are lretones containing at least one hydrogen atom on a carbon atom adjac-acetylprop-ionate, ethyl propionoacetate, methyl cent the carbonyl group, diketones containing at least one hydrogen atom on a carbon atom adjacent a carbonyl group, and ketocarboxylic esters containing at least one hydrogen atom adjacent the keto carbonyl group. The ketones and diketones containing at least two hydrogen atoms on the carbon atom adjacent the carbonyl group, and the ketocarboxylic esters containing at least two hydrogen atoms on the carbon atom adjacent the keto carbonyl group are especially useful in practicing the invention.
n-butyroacetate, phenyl'acetoacetate, ethyl decanoylacetate, methyl levulinate, ethyl levulinate, ethyl-a- (n-butyryl) -n-butyrate, diketones such as biacetyl (2,3-butanedione), acetylpropionyl, acetylisobutyryl, bipropionyl, bi-n-butyryl, acetylcaproyl, acetylacetone (2,4-pentanedione), 2,4- hexanedione, 2,4-heptanedione, 5-methyl-2,4-' hexanedione, benzoylacetone, benzoylethyl methyl ketone, benzoyl-n-butyl methyl ketone, benzoyliso-butyl methyl ketone, 1-phenyl-2,4-pentanedione, 3-methyl-2,4-pentanedione, 2,5-hexanedione, 6-methyl-2,5-heptanedione, 3,6-octanedione, lbenzoyl-2-butanone, 2,6-heptanedione, 1,3- cyclohexanedione, and the like.
The complex acid catalysts employed in the process of the invention may be prepared by thereaction of sulfuric acid on a. carboxylic acid or its anhydride. For example, when sulfuric acid and acetic anhydride are mixed in proper proportions, there is obtained acetyl sulfoacetic acid which has the following structural formula:
moles of acetic anhydride with one gram-mole of.
sulfuric acid (2) by reacting two gram-moles of acetic anhydride with one gram mole of sulfur trioxide and (3) by reacting two gram-moles of ketene with one gram-mole of sulfuric acid. When an aliphatic acid is formed as a by-product, as in above methods (1) and (2), the aliphatic acid is preferably first removed by distillation before use of the catalyst. While more than two gram-moles of acetic anhydride or ketene can be employed for each gram-mole of sulfuric acid or sulfur trioxide, the preferred ratio is two grammoles of acetic anhydride or ketene to one grammole of sulfuric acid or sulfur trioxide. The catalysts of the present invention are not to be confused with sulfoacetic acid or with sulfoacetic acid-acid addition products which function principally as condensation catalysts. formation of these latter compounds in situ. Regardless of how these catalysts are prepared, whether in situ or independently, they do not compare favorably as to yield and as to freedom from objectionable polymeric by-products with the complex acid catalysts of the present invention. Acetyl sulfoacetic acid is particularly efiicacious.
Prior art investigators have postulated the s 'The' following examples willserve" to illustrate' further the manner of practicing'the' invention.
, Preparation of acetyl .suljoacetic acid which formed was removed'bydistillation at 50] mm. pressure. The residu'e in the fiaskwas essentially pure acetyl sulfoa'c'etic acid.
Example 1 1 -acetoa:ybzttadiene-1,3
700 grams of crotonaldehyde, 1200 grams of isopropenyl acetate, 2 grams of acetyl sulfoacetic acid and 1 gram of copper acetate were mixed together in a distilling flask equipped with a short vigoreaux column and the mixture heated to gentle reflux. The excess isopropenyl acetate functioned as a diluent. 593 grams of acetone which formed in the reaction were removed over a period of 4 hours. The reaction mixture was then subjected to fractional distillation at reduced pressure. There was obtained a 96 per cent yield based on the crotonaldehyde of lacetoxy butadiene-l,3 boiling at 58 C. at 40 mm. pressure.
Example 2.-Alpha acetoxy styrene 2 gram-moles of acetophenone were heated with 2 gram-moles of isobutenyl acetate in a short still, in the presence of 0.5 gram of acetyl sulfoacetic acid. When 91 per cent of the theoretical quantity of methyl ethyl ketone, which formed in the reaction, had been removed by slowly distilling it off, the residue in the still was subjected to fractional distillation at reduced pressure. There was obtained an 87 per cent yield of alpha acetoxy styrene, boiling at 85 C. at 2 mm. pressure, based On the amount of isobutenyl acetate used.
Ewample 3.-2-acetomy butadiene-1,3
A mixture of 200 grams of methyl vinyl ketone, 400 grams of isopropenyl acetate, 0.6 gram of acetyl sulfoacetic acid and 0.5 gram of copper acetate Was heated to gentle reflux in a still. At the end of six hours, the theoretical quantity of acetone had been distilled off. Anhydrous sodium acetate was then added to the reaction mixture in sufficient quantity to neutralize the catalyst. The reaction mixture was then fractionally distilled. A yield of 275 grams of 2-acetoxy butadiene-1,3, boiling at 54 C. at 40 mm. pressure, was obtained. It had a refractive index (20/D) of 1.4421. This corresponds to a yield of 86 per cent based on the amount of methyl vinyl ketone used.
Example 4.-2-acetoary-3-methyl Zmtadiene-L3 A mixture of 200 grams of methyl isopropenyl ketone, 400 grams of isopropenyl acetate, 0.6 gram of acetyl sulfoacetic acid and 0.5 gram of copper acetate was heated to gentle reflux in a still. At the end of six hours, the theoretical quantity of acetone had been distilled off. Anhydrous sodium acetate was then added in amount suflicient to neutralize the catalyst. The reaction mixture was then fractionated. A yield of 283 grams of 2-acetoxy-3-methyl butadiene-L3, boiling at 62 C. at 40 mm. pressure, was obtained. It had a refractive index (20/D) of 1.4450. This corresponds to a yield of 95 per cent based on the amount of methyl isopropenyl ketone used.
Ezmmple 5.--Enol acetate'of ethyl acetoacetate 260 grams of ethyl acetoacetate, 300 grams of isopropenyl, aoetate and. 0.5 gram of propionyl sulfopropionic acid were mixed together and heatedto gentle reflux in a still. The theoretical quantity of acetone which formed in the reaction was distilled off in a period of 30 minutes of heatin After this time, the residue in the flask was fractionally distilled, at reduced pressure. A yield of 96,per cent of the theoretical, based on the amount of ethyl acetoacetate, of ethyl 2- acetoxy crotonate boiling at 10 mm. pressure was obtained. I
In the same manner illustrated above, acetaldehyde and isopropenyl acetate give vinyl acetate, propionaldehyde and isobutenyl acetate give l-acetoxy propane-1, n-butyraldehyde and isopropenyl acetate give n-butenyl acetate, phenylacetaldehyde and isopropenyl acetate give benzilidenemethyl acetate, diethyl ketone and isopropenyl acetate give 3-acetoxy pentene-2, cyclohexanone and isopropenyl acetate give cyclohexenyl acetate, acetyl acetone and isopropenyl acetate give 4-acetoxy-3-penten-2-one and 2,4-diacetoxy pentadiene-1,3, biacetyl and isopropenyl acetate give 2-acetoxy-1-buten-3-one and 2,3-diacetoxy 1,3-butadiene, ethyl pyruvate and isopropenyl acetate give ethyl a-acetoxyacrylate, etc.
Small amounts of water may be present in the reaction mixture without adversely affecting the process.
What I claim is:
1. A process for acylating enolizable organic compounds comprising heating, in the presence of an acid catalyst having the general formula:
wherein D and D1 represent divalent saturated aliphatic hydrocarbon groups of the same number of carbon atoms selected from the group consisting of a methylene group, an ethylene group and a propylene group, an unsaturated monocarboxylic ester selected from the group consisting of isopropenyl acetate, 2-acetoxy-butene-l, Z-acetoxy-pentene-l, 2-acetoxy-hexene- 1, Z-acetoxy-heptene-l, with an enolizable organic compound selected from the group consisting of aldehydes containing at least two carbon atoms and containing at least one enolizabl hydrogen atom on the carbon atom adjacent the carbonyl group, and aldehydes containing a carbon to carbon double bond conjugated with the double bond of the carbonyl group and containing at least one enolizable hydrogen atom on the carbon atom adjacent to one of the carbon atoms of the carbon to carbon double bond, ketones containing at least one hydrogen atom on a carbon atom adjacent to the carbonyl group and ketocarboxylic esters containing at least one hydrogen atom on the carbon atom adjacent the keto carbonyl group, and recovering the enol ester product which forms.
2. A process for acylating enolizable organic compounds comprising heating, in the presence of acetyl sulfoacetic acid, isopropenyl acetate With an aldehyde containing at least two carbon atoms and containing at least one hydrogen atom on the carbon atom adjacent the carbonyl group, and recovering the enol acetate of the aldehyde which forms.
3. A process for acylating crotonaldehyde comprising heating, in the presence of acetyl sulfoacetic acid, isopropenyl acetate with the crotonaldehyde, and recovering the l-acetoxy butadiene-1,3 which forms.
7?? 4.v,A-process for acylating enolizable organic compounds comprising heating, in the presence of acetyl sulfoacetic acid, isopropenyl acetate with a ketone which contains at least. one hydrogen atom on a carbon atom adjacent the carbony} group, and recovering the enol acetate of the ketone which forms.
' 5., A'process for acylating methyl vinyl ketone comprising heating, in the presence of acetyl snhoacetic acid, isopropenyl acetate with the methyl vinyl ketone, and recovering the 2- acetoxy' .butadiene-1,3 which forms.'
6. A process for acylating enolizable organic compounds comprisingheating, in the presence o1 -:propiony1 sulfopropionic acid, is'opropenyl acetate with a ketccarboxylic ester containing at least one hydrogen atom on the carbon atom adjacent the Kate carbonyl group, and recovering the enol acetate 01 the ketocarboxylic ester whichforms.
'ZL A process for acylating ethyl acetoacetate' comprising heating, in the presence of propionylsulfopropionic acid, isopropenyl acetate with the ethyl acetoacetate, and recovering the ethy1 2- No references cited.

Claims (1)

1. A PROCESS FOR ACYLATING ENOLIZABLE ORGANIC COMPOUNDS COMPRISING HEATING, IN THE PRESENCE OF AN ACID CATALYST HAVING THE GENERAL FORMULA:
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